Calculating Mass Flow Rate of Water in a Natural Draught Cooling Tower

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SUMMARY

The discussion focuses on calculating the mass flow rate of water entering a natural draught cooling tower, which experiences a 3% loss due to evaporation. The air enters at a volume flow rate of 4 m³/s, 10°C, and 50% relative humidity, while it exits saturated at 34°C. The water enters at 36°C, and participants suggest using the heat capacity (Cp) and energy balance equations to determine the mass flow rate, emphasizing the need to account for the evaporation loss. The key takeaway is that the moisture content of the air at inlet and outlet conditions can be used to derive the mass flow rate of water entering the tower.

PREREQUISITES
  • Understanding of natural draught cooling tower design principles
  • Knowledge of thermodynamics, specifically heat transfer and energy balance
  • Familiarity with psychrometric charts for air properties
  • Basic calculations involving mass flow rates and heat capacities
NEXT STEPS
  • Study the principles of natural draught cooling tower operation
  • Learn how to read and interpret psychrometric charts
  • Explore the calculation of mass flow rates using energy balance equations
  • Investigate the impact of evaporation losses on cooling tower efficiency
USEFUL FOR

Engineers, HVAC professionals, and anyone involved in the design and analysis of cooling systems will benefit from this discussion, particularly those focused on optimizing water flow rates in cooling towers.

chelonege
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A natural draught cooling tower is designed to have a 3% loss of the mass of the water entering the tower by evaporation into the atmosphere. Atmospheric air enters the tower at a volume flow rate of 4 m^3/s a temp of 10C and a relative humidity of 50%. Air leaves the tower in a saturated condition at a temp of 34C. The atm pressure is 0.995 bar. The water enters the tower at a temperature of 36C. Find the mass flow rate of water entering the tower.

The problem is I don't know how to find the h for the water at the outlet, any suggestions? Thx~
 
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Have you considered using CpΔT instead of enthalpy? This should be close enough if you use the average heat capacity between temperatures.
 
The point is if i don't know the outlet temp for water how will i be able to do CpT
 
I guess you need to assume standard cooling tower outlet conditions - 25 or 30 C maybe. Are there any design parameters to go by?
 
You know the inlet and outlet conditions for the air. You know the inlet conditions of the water, and that a certain amount of the water is lost due to evaporation. Don't you think you can determine how much water enters the tower based on the amount of energy required to heat the air leaving the cooling tower? The problem does not ask you to find the temperature of the cooled water, only how much enters initially.
 
But there's one equation and 2 unknowns. So the duty the air supplies, Q = water flow*Cp*(T1-T2). We don't have T2 and mass flow of water. We need to take a different path. We have to use the 3% loss in water mass that leaves the tower as steam.
 
i agree with Mrmiller, but how can I actually use the 3% and find H... I have been stuck here
 
You're not trying to find energy here, so I'm not sure what direction you guys are going with the problem. You have the inlet and outlet conditions of the air, so just read from a table or psych chart the moisture content at each, subtract, then convert to mass (then divide by 3%).
 

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